Medium optimization for the high yield production of single (+)-terrein by Aspergillus terreus strain PF26 derived from marine sponge Phakellia fusca

Terrein has potential application in the fields of medicine, cosmetology and agriculture, however, the chemical synthesis of terrein with single configuration is a difficult task, and the biosynthesis of terrein always results in low production (ca. 0.33–400 mg/L). In this study, we reported an Aspergillus terreus strain PF26 which could produce (+)-terrein on a high level. After the selection of a suitable basic medium, the component concentrations were optimized using Plackett–Burman design and response surface methodology. Consequently, an optimal medium containing 28.41 g glucose, 23.18 g maltose, 20.00 g mannitol, 8.52 g malt extract, 10.00 g monosodium glutamate 10.00 g NH₄Cl in 1 L ASW was obtained, and a high (+)-terrein production of 3.71 g/L fermentation broth was achieved, which represents the highest fermentation production of (+)-terrein to date. The result highlighted the industry's potential of A. terreus strain PF26 in the production of bioactive (+)-terrein on a large-scale.     

Enhanced production of (+)-terrein in fed-batch cultivation of Aspergillus terreus strain PF26 with sodium citrate

(+)-Terrein is a fungal metabolite with multiple biological activities, especially with great value in medicine. However, the mass production of single configuration terrein is still a big challenge. In this study, the effects of acetic acid, sodium acetate, citric acid and sodium citrate on the (+)-terrein production by Aspergillus terreus strain PF26 derived from marine sponge Phakellia fusca were investigated. Sodium citrate was selected for fed-batch cultivation because it showed the best effect on (+)-terrein production among the four regulators tested. As a result, 5.38 g/L (+)-terrein production was achieved by feeding 10 mM sodium citrate on the 3rd day in shake flask, which was 33.8 % higher than the control and represented the highest yield of (+)-terrein. In a 7.5-L stirred bioreactor, 2.58 g/L of (+)-terrein production was achieved by the feeding of 10 mM sodium citrate on the 8th day. The results from this study lay a basis for the high-yield production of (+)-terrein by fermentation.     

Operating conditions optimization for (+)-terrein production in a stirred bioreactor by Aspergillus terreus strain PF-26 from marine sponge Phakellia fusca

Terrein is a fungal metabolite with application values in the fields of medicine, cosmetology, and agriculture. However, mass production of single configuration terrein is still a big challenge. In this study, operating factors such as inoculation, agitation speed, aeration rate, pH control, and nutrient feeding were preliminarily optimized to improve the (+)-terrein production in the 5-L stirred bioreactor from the marine sponge-derived fungus Aspergillus terreus PF-26. Spore inoculation, low agitation speed, and aeration rate were proved to be suitable for A. terreus PF-26 to produce (+)-terrein in the stirred bioreactor. At 50?rpm agitation speed and 0.33?vvm aeration rate, 2.68?g/L (+)-terrein was achieved by feeding twofold concentrated maltose and glucose medium on the sixth day and controlling pH at 4.5 from the fourth day. This study lays foundation for the mass production of (+)-terrein by the marine filamentous A. terreus strain PF-26 in the stirred bioreactor.     

Continuous 2-keto-gluconic acid (2KGA) production from corn starch hydrolysate by Pseudomonas fluorescens AR4

A continuous fermentation process for 2-keto-gluconic acid (2KGA) production from cheap raw material corn starch hydrolysate was developed using the strain Pseudomonas fluorescens AR4. The dilution rate and feeding glucose concentration had a significant effect on the cell concentrations, glucose utilization and 2KGA production performance. The optimal operating factors were obtained as: 0.065 h⁻¹ of dilution rate, 180 g/L of feeding glucose concentration, and 16 h of batch fermentation time as the starting point. Under these conditions, the steady state had the 135.92 g/L of produced 2KGA concentration, 8.83 g/L.h of average volumetric productivity, and 0.9510 g/g of yield. In conclusion, the proposed efficient and stable continuous fermentation process for 2KGA production by the strain P. fluorescens AR4 is potentially competitive for industrial production from corn starch hydrolysate in terms of 2KGA productivity and yield.     

Enhancing GDP-fucose production in recombinant Escherichia coli by metabolic pathway engineering

Guanosine 5′-diphosphate (GDP)-fucose is the indispensible donor substrate for fucosyltransferase-catalyzed synthesis of fucose-containing biomolecules, which have been found involving in various biological functions. In this work, the salvage pathway for GDP-fucose biosynthesis from Bacterioides fragilis was introduced into Escherichia coli. Besides, the biosynthesis of guanosine 5′-triphosphate (GTP), an essential substrate for GDP-fucose biosynthesis, was enhanced via overexpression of enzymes involved in the salvage pathway of GTP biosynthesis. The production capacities of metabolically engineered strains bearing different combinations of recombinant enzymes were compared. The shake flask fermentation of the strain expressing Fkp, Gpt, Gmk and Ndk obtained the maximum GDP-fucose content of 4.6 ± 0.22 μmol/g (dry cell mass), which is 4.2 fold that of the strain only expressing Fkp. Through fed-batch fermentation, the GDP-fucose content further rose to 6.6 ± 0.14 μmol/g (dry cell mass). In addition to a better productivity than previous fermentation processes based on the de novo pathway for GDP-fucose biosynthesis, the established schemes in this work also have the advantage to be a potential avenue to GDP-fucose analogs encompassing chemical modification on the fucose residue.     

Mixed culture of Saccharomyces cerevisiae and Acetobacter pasteurianus for acetic acid production

Mixed culture of Saccharomyces cerevisiae and Acetobacter pasteurianus was carried out for high yield of acetic acid. Acetic acid production process was divided into three stages. The first stage was the growth of S. cerevisiae and ethanol production, fermentation temperature and aeration rate were controlled at 32 °C and 0.2 vvm, respectively. The second stage was the co-culture of S. cerevisiae and A. pasteurianus, fermentation temperature and aeration rate were maintained at 34 °C and 0.4 vvm, respectively. The third stage was the growth of A. pasteurianus and production of acetic acid, fermentation temperature and aeration rate were controlled at 32 °C and 0.2 vvm, respectively. Inoculation volume of A. pasteurianus and S. cerevisiae was 16% and 0.06%, respectively. The average acetic acid concentration was 52.51 g/L under these optimum conditions. To enhance acetic acid production, a glucose feeding strategy was subsequently employed. When initial glucose concentration was 90 g/L and 120 g/L glucose was fed twice during fermentation, acetic acid concentration reached 66.0 g/L.     

Enhancement of pilot scale production of l(+)-lactic acid by fermentation coupled with separation using membrane bioreactor

Traditional batch fermentation leads to a higher energy consumption and lower production capability because of longer culture time. In this work, a pilot scale bioreactor composed of a 3000 L fermentor and external ceramic microfiltration equipment was used to perform cell-recycle fermentation. Repeat feeding medium was also used to relieve the substrate inhibition. In such pilot system, the maximum yield and productivity of l(+)-lactic acid production reached 157.22 ± 3.42 g/L and 8.77 ± 0.15 g/L/h which were 4.23% and 315.64% higher than those of batch fermentation, respectively, when equal amount of sugar was consumed. The cost of l(+)-lactic acid production was successfully reduced about two-thirds by the increase of yield and productivity. 12 rounds of cell-recycle fermentations were successfully achieved in the pilot system. The membrane filtration productivity reached to 61.27 ± 2.74 L/m²/h which increased 172.80%, while the cell damaging rate dropped to 3.88 ± 0.18% which decreased 85.77%, compared with those of the ultrafiltration. Furthermore, the ceramic microfiltration membrane showed advantages in tolerance for the temperature, pressure and acid, compared with the organic ultrafiltration membrane. The experimental results indicated that the method could give a reference for low cost production of l(+)-lactic acid in an industrial scale.     

The influence of culturing environments on lovastatin production by Aspergillus terreus in submerged cultures

The effect of the changes of culturing environments of Aspergillus terreus on lovastatin production was investigated in the study. A relatively low supplement of dissolved O₂ (DO) by the fungus almost stopped performing product formation. With the DO controlled at 20%, lovastatin production using a 5-l fermenter enhanced by 38%, biomass production decreased by 25% and sugar utilization increased by 18%, as compared with the shaking-flask culture. Meanwhile, an average diameter 0.95 mm of compact pellets was found. We thus concluded that pellet formation with a narrow size distribution dominated lovastatin production by A. terreus, which was closely affected by the relatively saturated level of DO. Nevertheless, manipulating the broth pH at 5.5–7.5 starting from 48 h provided no benefit to product formation although biomass production was reduced largely. In the part of work, a pH/DO interaction was also confirmed.A simple temperature-shift method (28–23 °C) was proved surprisingly valuable to the fermentation process. Such experiments showed that the maximum of lovastatin production was further enhanced by 25% (572 mg/l at day 10) in comparison with that when the fungus was cultured at 28 °C. The timing to initiate the temperature-shift (96 h) corresponded to that of pellet formation and the subsequent core compactness. Hence, it was found that lovastatin production by A. terreus favored sub-optimal growth conditions.     

Isolation and identification of a novel Rhodococcus sp. ML-0004 producing epoxide hydrolase and optimization of enzyme production

Rhodococcus sp. ML-0004, a novel strain for producing epoxide hydrolase, was isolated from soil in this study. The epoxide hydrolase can catalyze the stereo-specific hydrolysis of cis-epoxysuccinic acid to generate l(+)-tartaric acid. By examining physiological, biochemical characteristics and comparing its 16S rDNA gene sequence, it was identified as Rhodococcus opacus, and named R. opacus ML-0004. The optimal conditions for epoxide hydrolase production from R. opacus ML-0004 were also investigated. Propanediol and (NH₄)₂SO₄ were selected as carbon source and nitrogen source, respectively, for the production of R. opacus ML-0004 epoxide hydrolase. The optimal conditions for epoxide hydrolase production were fermentation temperature = 28 °C, pH 7.0, and cultivation time = 26 h. Under these conditions, the maximum epoxide hydrolase activity reached 10.5 U mL⁻¹.     

Production enhancement of Rhizopus arrhizus lipase by feeding oleic acid

A strategy for Rhizopus arrhizus lipase production enhancement by feeding oleic acid was developed. The oleic acid was proved to have strong inducing effect on lipase production, but high concentration oleic acid could repress lipase production. The decrease rate of oleic acid concentration using peanut oil as initial carbon source was figured out according to the change of oleic acid concentration in the fermentation broth. Our feeding strategy designed based on the decrease rate of oleic acid could avoid the repression of lipase production that is caused by high concentration of oleic acid in the fermenting liquor, and this strategy worked as a new feeding method showing excellent performance. The maximum lipase activity was gained by feeding dilute oleic acid every 12 h starting at 60 h, which maintained the oleic acid concentration around 18 mg/L, and the lipase activity was 31% higher than that of no feeding.     

Correlation of pigment production with mycelium morphology in extractive fermentation of Monascus anka GIM 3.592

Extractive fermentation with nonionic surfactants is a potential method for producing Monascus pigments. In this study, the correlation between mycelium morphology and pigment production was investigated in extractive fermentation of Monascus anka GIM 3.592. The results demonstrated that pigment biosynthesis was associated with mycelial morphology and the accumulation of granular inclusions in cells. The physiological status in terms of hyphal and pellet diameters exhibited an excellent correlation with pigment accumulation, especially the yield of extracellular pigment in extractive fermentation (r > 0.85, p < 0.05). Nonionic surfactants could reduce pigment yield by influencing the morphology of hyphae and mycelium pellets. High yields of both intracellular and extracellular pigments could be achieved by controlling variations in hyphal diameters in two-stage extractive fermentation. Moreover, continuous extractive fermentation led to stable pigment production, with a relatively high productivity of total pigments reaching 72.3 AU/day. This study proposed a simple method for monitoring pigment biosynthesis in extractive fermentation using mycelium morphology as an indicating factor.     

Use of different carbon sources in cultivation of recombinant Pichia pastoris for angiostatin production

To improve the growth of recombinant Pichia pastoris with a phenotype of Mut^S and expression of angiostatin, the effects of glycerol, sorbitol, acetate and lactic acid which were, respectively, added together with methanol in the expression phase, were studied in a 5-l fermentor. Methanol concentration was automatically controlled at 5 g/l by a methanol monitor and control system, while the feeding of the other carbon source was manually adjusted. The angiostatin production level was 108 mg/l when glycerol was added at an initial rate of 2.3 g/h and gradually increased to 9.9 g/h within an induction period of 96 h. The angiostatin concentration was 141 mg/l as sorbitol was used, while only 52 mg/l were obtained on acetate. The highest angiostatin production of 191 mg/l was achieved as lactic acid was used; whose feeding rate was gradually increased from 2.6 to 11.3 g/h. Lactic acid accumulated during the induction phase and reached 6.3 g/l at the end of fermentation. However, the accumulation of lactic acid did not interfere with angiostatin production, indicating that lactic acid to be a non-repressive carbon source. The average productivity and specific productivity of angiostatin obtained on lactic acid and methanol were, respectively, 2.96 and 0.044 mg/(g h), 1.7- and 2.5-fold of those obtained in the fermentation fed with glycerol and methanol.     

5-Aminolevulinic acid production in engineered Corynebacterium glutamicum via C5 biosynthesis pathway

ALA (5-aminolevulinic acid) is an important intermediate in the synthesis of tetrapyrroles and the use of ALA has been gradually increasing in many fields, including medicine and agriculture. In this study, improved biological production of ALA in Corynebacterium glutamicum was achieved by overexpressing glutamate-initiated C₅ pathway. For this purpose, copies of the glutamyl t-RNA reductase HemA from several bacteria were mutated by site-directed mutagenesis of which a HemA version from Salmonella typhimurium exhibited the highest ALA production. Cultivation of the HemA-expressing strain produced approximately 204 mg/L of ALA, while co-expression with HemL (glutamate-1-semialdehyde aminotransferase) increased ALA concentration to 457 mg/L, representing 11.6- and 25.9-fold increases over the control strain (17 mg/L of ALA). Further effects of metabolic perturbation were investigated, leading to penicillin addition that further improves ALA production to 584 mg/L. In an optimized flask fermentation, engineered C. glutamicum strains expressing the HemA and hemAL operon produced up to 1.1 and 2.2 g/L ALA, respectively, under glutamate-producing conditions. The final yields represent 10.7- and 22.0-fold increases over the control strain (0.1 g/L of ALA). From these findings, ALA biosynthesis from glucose was successfully demonstrated and this study is the first to report ALA overproduction in C. glutamicum via metabolic engineering.     

Epigenetic modifier-induced biosynthesis of novel acetylenic sterols from Cladosporium colocasiae

The addition of an HDAC inhibitor, suberoylanilide hydroxamic acid (SBHA), to the culture medium of Cladosporium colocasiae, dramatically altered its metabolic profiles. Analysis of the culture broth extract led to the isolation of two new acetylenic sterols (1–2). The isolated compounds were further evaluated for their cytotoxic and antibacterial activities. Compound 1 showed activity against Bacillus subtilis, affording a zone of inhibition of 12 mm at 100 μg/disk. However, none of them showed noticeable growth inhibitory effects.     

Stepwise metabolic engineering of Gluconobacter oxydans WSH-003 for the direct production of 2-keto-l-gulonic acid from d-sorbitol

2-Keto-l-gulonic acid (2-KLG), the direct precursor of vitamin C, is currently produced by a two-step fermentation route from d-sorbitol. However, this route involves three bacteria, making the mix-culture system complicated and redundant. Thus, replacement of the conventional two-step fermentation process with a one-step process could be revolutionary in vitamin C industry. In this study, different combinations of five l-sorbose dehydrogenases (SDH) and two l-sorbosone dehydrogenases (SNDH) from Ketogulonicigenium vulgare WSH-001 were introduced into Gluconobacter oxydans WSH-003, an industrial strain used for the conversion of d-sorbitol to l-sorbose. The optimum combination produced 4.9 g/L of 2-KLG. In addition, 10 different linker peptides were used for the fusion expression of SDH and SNDH in G. oxydans. The best recombinant strain (G. oxydans/pGUC-k0203-GS-k0095) produced 32.4 g/L of 2-KLG after 168 h. Furthermore, biosynthesis of pyrroloquinoline quinine (PQQ), a cofactor of those dehydrogenases, was enhanced to improve 2-KLG production. With the stepwise metabolic engineering of G. oxydans, the final 2-KLG production was improved to 39.2 g/L, which was 8.0-fold higher than that obtained using independent expression of the dehydrogenases. These results bring us closer to the final one-step industrial-scale production of vitamin C.     

An engineering Escherichia coli mutant with high succinic acid production in the defined medium obtained by the atmospheric and room temperature plasma

Escherichia coli BA002, the ldhA and pflB deletion strain, cannot utilize glucose in nutrient-rich or minimal media anaerobically. Co-expression of heterologous pyruvate carboxylase and nicotinic acid phosphoribosyltransferase in BA002 resulted in a significant increase in cell mass and succinic acid production. Nevertheless, the resultant strain, BA016, still could not grow in a defined medium without tryptone and yeast extract. To solve the problem, a novel atmospheric and room temperature plasma mutation method was employed to generate mutants which can grow in the defined medium. A mutant designated as LL016 was observed to be the best strain that regained the capacity of cell growth and glucose utilization in a defined medium anaerobically. After 120 h of fermentation in the defined medium, 35.0 g/L of glucose was consumed to generate 25.2 g/L of succinic acid. Furthermore, with the highest glucose consumption rate in the dual-phase fermentation, the yield of succinic acid in LL016 reached 0.87 g/g, which was higher than that observed in other strains. From an industrial standpoint, the defined medium is much cheaper than LB medium, which shows a great potential usage for the economical production of succinic acid by LL016.     

Enhanced production of valienamine by Stenotrophomonas maltrophilia with fed-batch culture in a stirred tank bioreactor

Valienamine is an important medicinal intermediate with broad use in the synthesis of some stronger α-glucosidase inhibitors. In order to improve valienamine concentration in the fermentation broth and make the downstream treatment easy, a fed-batch process for the enhanced production of valienamine by Stenotrophomonas maltrophilia in a stirred tank bioreactor was developed. Results showed that supplementation of validamycin A in the process of cultivation could increase the valienamine concentration. One-pulse feeding was observed to be the best strategy. The maximum valienamine concentration of 2.35 g L⁻¹ was obtained at 156 h when 86.4 g of validamycin A was added to a 15-L bioreactor containing 8 L fermentation medium with one-pulse feeding. The maximum valienamine concentration had a great improvement and was increased above 100% compared to batch fermentation in the stirred tank bioreactor. The pH-controlled experiments showed that controlling the pH in the process of one-pulse feeding fermentation had not obvious effect on the production of valienamine.     

Fermentation process for continuous production of succinic acid in a fibrous bed bioreactor

Succinic acid (SA) was produced from Actinobacillus succinogenes with high cell density by continuous fermentation using fibrous bed bioreactor (FBB). The effects of feeding glucose concentration, dilution rate, and pH on continuous production of SA were examined to achieve an efficient and economical bioprocess. The optimum feeding glucose concentration, dilution rate, and pH were 80 g/L, 0.05 1/h, and 6.0–6.5, respectively. A SA concentration of 55.3 ± 0.8 g/L, productivity of 2.77 ± 0.04 g/L/h, and yield of 0.8 ± 0.02 g/g were obtained, and the continuous fermentation exhibited long-term stability for as long as 18 days (440 h) with no obvious fluctuations in both SA and biomass levels. The Jerusalimsky equation for the specific rate of SA production presented the inhibition phenomenon of the product, demonstrating that 60 g/L SA might be a critical concentration in this continuous FBB system. The results obtained could be beneficial for future fermentor designs and improvements in SA production.